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Process Equipment and Plant Design

Process Equipment and Plant Design
The safe height (h) to diameter (d) ratio (i.e., h/d) for liquid/petro fuel storage tank of capacity more than 45 kilolitres is less than

3
3.5
2
1

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Process Equipment and Plant Design
For a given design of bubble cap, the number of bubble caps to be used per tray is set by the

Plate spacing
All of these
Allowable gas velocity through the slots
Diameter of the column

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Process Equipment and Plant Design
Bubble cap diameter used for the distillation column having diameter ranging from 1.5 to 4.5 metres is about __________ mm.

100
50
150
10

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Process Equipment and Plant Design
Le/D for fully open globe value may be around

75
25
10
300

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Process Equipment and Plant Design
Nominal size of a pipe is an indication of its __________ diameter.

Approximate
None of these
Outer
Inner

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Process Equipment and Plant Design
Accidents in chemical plants are mostly due to

Inadequate equipment design
Faulty operating procedures
Improper layout of the equipments
Failure of equipments

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